  
 |  |       | |  Projects, Compliance Energy Corporation | | | | | | | | | Proximate Analysis | | | Ultimate Analysis | | Moisture | | 10.0% | | Carbon | 62.7% | | Residual Moisture | | 3.0% | | Hydrogen | 4.8% | | Ash | | 12.0% | | Nitrogen | 1.3% | | Volatile Matter | | 32.5% | | Oxygen | 13.6% | | Fixed Carbon | | 45.0% | | Sulphur | 0.5% | | Sulphur | | 0.5% | | Ash | 12.0% | | | | | | | | | Hardgrove grindablity index | | 45-59 | | Approx. Sulphur Breakdown | | | Free Swelling Index | | 0 to 1.0 | | Organic | 0.46% | | Gross Heat Value | kcal/kg | 6,000 | | Pyritic | 0.09% | | | Btu/lb | 10,800 | | Sulphate | 0.01% | | | | | | | | | Ash Fusibility | | | Ash Analysis | | Reducing Condition | | Deg. Centigrade | | SiO2 | 70.5% | | Initial Deformation | | 1,288 | | Al2O3 | 16.2% | | Softening Temp. | | 1,399 | | Fe2O3 | 5.1% | | Hemisphere Temp | | 1,435 | | CaO | 0.7% | | Fluid Temp | | 1,482 | | MgO | 0.5% | | | | | | Na2O | 0.6% | | Oxidizing Conditions | | | K2O | 0.6% | | Initial Deformation | | 1,354 | | TiO2 | 0.7% | | Softening Temp. | | 1,438 | | P2O5 | 0.2% | | Hemisphere Temp | | 1,460 | | SO3 | 0.4% | | Fluid Temp | | 1,482 | | Undetermined | 4.5% | | | | | | | | | Screen Size | %
Weight | Cumm. %
Passing | | | | | 2 x 1 | 22.6% | 100.0% | | | | | 1 x ¾ | 8.3% | 77.4% | | | | | ¾ x ½ | 10.9% | 69.16% | | | | | ½ x ¼ | 17.9% | 58.3% | | | | | ¼ x 8M | 19.7% | 40.3% | | | | | 8M x 0 | 20.7% | 20.7% | | | | | |
